DE1521065C3 - Acid galvanic nickel bath for the deposition of decorative fine-grained, satin to high-gloss coatings with improved corrosion resistance - Google Patents
Acid galvanic nickel bath for the deposition of decorative fine-grained, satin to high-gloss coatings with improved corrosion resistanceInfo
- Publication number
- DE1521065C3 DE1521065C3 DE1521065A DE1521065A DE1521065C3 DE 1521065 C3 DE1521065 C3 DE 1521065C3 DE 1521065 A DE1521065 A DE 1521065A DE 1521065 A DE1521065 A DE 1521065A DE 1521065 C3 DE1521065 C3 DE 1521065C3
- Authority
- DE
- Germany
- Prior art keywords
- oxalates
- nickel
- oxalate
- bath
- thorium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D15/00—Electrolytic or electrophoretic production of coatings containing embedded materials, e.g. particles, whiskers, wires
- C25D15/02—Combined electrolytic and electrophoretic processes with charged materials
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- Y10S428/00—Stock material or miscellaneous articles
- Y10S428/922—Static electricity metal bleed-off metallic stock
- Y10S428/923—Physical dimension
- Y10S428/924—Composite
- Y10S428/926—Thickness of individual layer specified
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- Y10S428/00—Stock material or miscellaneous articles
- Y10S428/922—Static electricity metal bleed-off metallic stock
- Y10S428/9265—Special properties
- Y10S428/927—Decorative informative
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- Y10S428/9335—Product by special process
- Y10S428/934—Electrical process
- Y10S428/935—Electroplating
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- Y10T428/12028—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, etc.]
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- Y10T428/12639—Adjacent, identical composition, components
- Y10T428/12646—Group VIII or IB metal-base
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- Y10T428/12771—Transition metal-base component
- Y10T428/12778—Alternative base metals from diverse categories
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- Y10T428/12771—Transition metal-base component
- Y10T428/12806—Refractory [Group IVB, VB, or VIB] metal-base component
- Y10T428/12826—Group VIB metal-base component
- Y10T428/12847—Cr-base component
- Y10T428/12854—Next to Co-, Fe-, or Ni-base component
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/12771—Transition metal-base component
- Y10T428/12861—Group VIII or IB metal-base component
- Y10T428/12944—Ni-base component
Description
3 43 4
Überzug, wenn ihnen der übliche dünne abschließende 1 bis 20 g/l Bariumsulfat oder Strontiumsulfat dem Chromüberzug von etwa 0,25 Mikron aufgebracht Bad zugesetzt sind. Mischungen der feinen Kieselsäure wird. Ein verbesserter Korrosionsschutz wird sogar mit Ceroxalaten und/oder Magnetit ergeben ebenfalls mit den dekorativen Überzügen (mit einem ab- sehr gute Ergebnisse, und die günstigsten Ergebnisse schließenden Chromüberzug einer Stärke von weniger 5 werden erhalten bei Konzentrationen von 20 bis 50 g/l als etwa 5 Mikron) aus Bädern gewonnen, die nur Kieselsäure und 5 bis 50 g/l Magneteisenoxid. Mietwa 0,5 g/l Oxalatpartikeln enthalten. Die Oxalat- schungen von Ceroxalaten und Oxalaten der Seltenen pulver sind bei niedrigeren Konzentrationen eher Erden mit Magnetitpulver ergeben sehr gute Ergebwirksamer als beispielsweise die Oxide. nisse, insbesondere bei 1 bis 20 g/l Oxalaten SeltenerCoating, if you want the usual thin final 1 to 20 g / l barium sulfate or strontium sulfate Chrome plating of approximately 0.25 microns is applied to the bath. Mixtures of fine silica will. Improved protection against corrosion is also obtained even with cerium oxalates and / or magnetite with the decorative coatings (with an ab- very good results, and the most favorable results A final chrome coating of a thickness of less than 5 is obtained at concentrations of 20 to 50 g / l than about 5 microns) obtained from baths containing only silica and 5 to 50 g / l magnetic iron oxide. Rental wa Contains 0.5 g / l oxalate particles. The oxalates of cerium oxalates and oxalates of the rare ones In the case of lower concentrations, powders tend to be earths with magnetite powder giving very good results than, for example, the oxides. Nits, especially with 1 to 20 g / l oxalates, are less common
Die größtmögliche Verbesserung im Korrosions- io Erden auf 5 bis 50 g/l Magneteisenoxid, schutz der weniger leicht zugänglichen ausgenommenen Thoriumfluorid bei alleiniger Verwendung als Fest-Bereiche der Gegenstände wird erreicht, wenn etwa stoff in Hoch- und Halbglanznickelbädern ermöglicht 10 bis 100 g/l der !einteiligen Feststoffe in den Nickel- einen Überzug von ähnlich hoher Korrosionsbeständigbädern dispergiert werden. Eine weitere Erhöhung keit nach der Verchromung, wie sie bei Verwendung der Konzentration verbessert nicht den schon aus- 15 der Oxalat erzielt wird. Auch bei Verwendung von gezeichneten Korrosionswiderstand, wenn ein. ab- Thoriumfluoborat allein oder in Mischung mit schließender dünner Chromüberzug aufgebracht wird. Thoriumtetrafluorid oder Thoriumfluosilicat als Fest-Überzüge, die aus Bädern erzielt werden, welche stoffe werden gute Ergebnisse erzielt. Bei Verwendung höhere Feststoff konzentrationen enthalten, werden in glänzenden Nickelbädern verursacht jedoch Magnebis-zu einem Punkte trüber, bei dem eine weitere ao tit-Pulver eine viel größere Trübung in dem Überzug, Zunahme in der Konzentration keine weitere Ver- ergibt aber einen Überzug von überlegener Korroänderung im Aussehen des Nickel Überzuges bei sionsbeständigkeit. Ein glänzender Überzug mit gegebenen Arbeitsbedingungen vonstatten geht. geringster Trübung und ausgezeichneten Korrosions-Die oben bezeichneten feinteiligen Feststoffe können Schutzeigenschaften wird mit mikrofeinem Kieselim Gemisch mit anderen feinen nichtmetallischen und 25 säurepulver bei einer Konzentration von 40 bis -50 g/l in dem Bad unlöslichen Pulvern einer durchschnitt- in den Hochglanznickelbädern erzielt. Wie erwähnt, liehen Partikelgröße von etwa 5 Mikron und weniger können auch Kombinationen von Feststoffen erfolgverwendet werden, z. B. Mischungen von Nickel- reich eingesetzt werden. Der Zusatz von Thoriumoxalatpulver mit feinem Kieselsäurepulver, feinem fluorid in einer Menge von 1 bis 10 g/l, Magnetit mit Nickelkarbonatpulver oder feinem Calciumfluorid- 30 0,5 g/l und Ceroxalat bei 1 bis 10 g/l mit 40 bis 50 g/l pulver. Ausgezeichnete Kombinationen feiner Feststoffe Kieselsäure in dem Bad ermöglicht die Erzielung eines sind Nickeloxalat und Siliciumdioxid, mit oder ohne feinkörnigen Überzuges, welcher anschließend mit Bariumoxalat, Strontiumoxalat oder Strontiumsulfat. Chrom einer Stärke von/ weniger als' 5 Mikron über-Diese Mischungen werden am besten in folgender zogen, eine hervorragende Korrosionsbeständigkeit Weise hergestellt: Es wird eine Lösung aus Natrium- 35 insbesondere dann aufweist, wenn der feinkörnige oxalat, Magnesiumoxalat oder Oxalsäure (1% bis Überzug über einem halbglänzenden und/oder hoch-Sättigung) von einem porösen Siliciumdioxydpulver glänzenden Nickelüberzug aufgebracht wird, absorbiert, vorzugsweise Philadelphia Quarz, einer In den folgenden Beispielen sind die unteren Festmikrofeinen Kieselsäure, oder einem kieselsäure- stoff-Konzentrationen von etwa 0,5 g/l bis etwa 50 g/l ähnlichen Pulver, welches eine maximale Partikel- 40 am besten für hochglänzende Überzüge aus Glanzgröße von 0,02 Mikron hat, jedoch im allgemeinen nickelbädern geeignet und können somit zweckmäßig in agglomerierter Form von Kapseln von etwa für dünne Überzüge von etwa 0,25 bis etwa 5 Mikron , 1,5 Mikron durchschnittlicher Partikelgröße vorliegt. Dicke über einem üblichen glänzenden oder halb-:· ) Die überschüssige Flüssigkeit wird von dem Kiesel- glänzenden Nickelüberzug verwendet werden, um säurepulver abgelassen, und das letztere wird dem 45 nach dem anschließenden dünnen Chromüberzug Hoch- oder Halbglanznickelbad zugesetzt. Die Kiesel- einen hochkorrosionsbeständigen Glanzüberzug zu säure ist nicht nur selbst vorteilhaft und wirksam an erzielen. Es wurden beschleunigte Korrosionsteste der Bildung des dekorativen feinkörnigen Überzuges unter Anwendung der CASS- und Corrodkotebeteiligt, sondern modifiziert auch die Bildung und das Vorschriften durchgeführt, und es wurden mit üblichen Wachstum der Nickeloxalatniederschläge. Wenn die 5° Hoch- und Halbglanznickelüberzügen von nur 15 oder Kieselsäure mit Barium oder Strontiumchlorid im- 20 Mikron unter einem dünnen Überzug von beispielsprägniert und dann mit Nickeloxalatpulver gemischt weise 0,25 bis 2,5 Mikron Dicke aus den in den oder mit Natriumoxalat imprägniert und dann den folgenden Beispielen beschriebenen Bädern und einem Hochglanzbädern zugesetzt wird, werden ausgezeich- abschließenden Chromüberzug von 0,25 Mikron Dicke nete Ergebnisse hinsichtlich der Korrosionsbeständig- 55 viele Zyklen durchlaufen. Im Gegensatz dazu haben keit erreicht, wenn der aus dem Bad gewonnene Über- . Überzüge mit üblichem glänzendem Nickel der zug mit einem Chromüberzug von weniger als 5 Mikron gleichen Gesamtüberzugsstärke und dem gleichen Dicke versehen wird. Andere im Handel erhältliche abschließenden dünnen Chromüberzug einen einzigen feine Kieselsäuren in Form von Agglomeraten von Zyklus überstanden.The greatest possible improvement in corrosive earth to 5 to 50 g / l magnetic iron oxide, protection of the less easily accessible exempt thorium fluoride when used alone as solid areas of the objects is achieved if, for example, material in high and semi-gloss nickel baths allows 10 to 100 g / The one-part solids are dispersed in the nickel coating with a similarly high corrosion resistance bath. A further increase in speed after chrome plating, as it does when using the concentration, does not improve that which is already achieved from the oxalate. Even when using drawn corrosion resistance, if a. ab- Thorium fluorate is applied alone or in a mixture with a thin chrome coating. Thorium tetrafluoride or thorium fluosilicate as solid coatings, which are obtained from baths, which materials are good results. When used, higher solids concentrations are caused in shiny nickel baths, however, Magnebis to a point where another ao tit powder produces a much greater turbidity in the coating, an increase in the concentration does not result in any further loss but a coating of superior Corrosion change in the appearance of the nickel coating with sion resistance. A glossy coating takes place with given working conditions. Lowest turbidity and excellent corrosion protection properties is achieved with microfine silica in a mixture with other fine non-metallic and acid powders at a concentration of 40 to -50 g / l in the bath insoluble powders of an average in the high-gloss nickel baths. As mentioned, given particle sizes of about 5 microns and less, combinations of solids can also be used successfully, e.g. B. Mixtures of nickel-rich can be used. The addition of thorium oxalate powder with fine silica powder, fine fluoride in an amount of 1 to 10 g / l, magnetite with nickel carbonate powder or fine calcium fluoride - 30 0.5 g / l and cerium oxalate at 1 to 10 g / l with 40 to 50 g / l powder. Excellent combinations of fine solids Silicic acid in the bath enables one to achieve a are nickel oxalate and silicon dioxide, with or without a fine grain coating, which is then coated with barium oxalate, strontium oxalate or strontium sulfate. Chromium less than 5 microns thick- These mixtures are best prepared in the following way, with an excellent corrosion resistance: A solution of sodium is obtained, especially when the fine-grained oxalate, magnesium oxalate or oxalic acid (1% until coating is applied over a semi-glossy and / or high-saturation) of a porous silicon dioxide powder glossy nickel coating, absorbed, preferably Philadelphia quartz, a In the following examples, the lower solid microfine silica, or a silica concentration of about 0.5 g / l to about 50 g / l similar powder, which has a maximum particle 40 best for high-gloss coatings of a gloss size of 0.02 microns, but is generally suitable for nickel baths and can thus be conveniently used in agglomerated form of capsules of about for thin Coatings of about 0.25 to about 5 microns, 1.5 microns average particle size are present. Thickness above a usual shiny or semi-glossy : ·) The excess liquid from the siliceous nickel coating is used to drain acid powder, and the latter is added to the 45 after the subsequent thin chrome coating high or semi-gloss nickel bath. The silica a highly corrosion-resistant gloss coating to acid is not only beneficial and effective in achieving it. Accelerated corrosion tests of the formation of the decorative fine-grained coating using the CASS and Corrodkote were involved, but also modified the formation and prescriptions were carried out, and the normal growth of nickel oxalate precipitates was carried out. If the 5 ° high and semi-gloss nickel coatings of only 15 or silica with barium or strontium chloride im- 20 microns under a thin coating of for example impregnated and then mixed with nickel oxalate powder, 0.25 to 2.5 microns thick from the in or impregnated with sodium oxalate and then added to the baths described in the following examples and a high-gloss bath, excellent results in terms of corrosion resistance will be passed through many cycles. In contrast, have achieved speed when the excess gained from the bath. Plating with the usual bright nickel which is given a chrome plating of less than 5 microns of the same total plating thickness and the same thickness. Other commercially available final thin chromium plating survived a single fine silica in the form of agglomerates of cycle.
Durchschnitts-Partikelgrößen von wenigstens 5Mikron, 60 Die folgenden Beispiele erläutern die Erfindung, welche die Neigung haben, in bewegten Bädern inAverage particle sizes of at least 5 microns, 60 The following examples illustrate the invention, which have the tendency in moving baths in
Agglomerate einer Größe von etwa 1,5 Mikron aus- B e i s d i e I I einanderzubrechen, bringen auch befriedigende Ergebnisse. Ein Feststoffgemisch aus Kieselsäure, Nickel- Das Bad wurde durch Luft bewegt oxalat oder ohne Barium- oder Strontiumsulfat einer 65 g/l Durchschnitts-Partikelgröße von 5 Mikron und weni- Nickeloxalat (durchschnittliche Parger bringen optimale Ergebnisse, wenn 10 bis 50 g/l tikelgröße, 5 Mikron und weniger) 10 bis 100 feine Kieselsäure, 0,5 bis 20 g/l Nickeloxalat und NiSO4 · 6 H2O 200 bis 300Agglomerates about 1.5 microns in size to break apart the II also give satisfactory results. A solid mixture of silica, nickel- The bath was moved through air oxalate or without barium or strontium sulfate an average particle size of 65 g / l of 5 microns and less nickel oxalate (average Parger bring optimal results when 10 to 50 g / l particle size , 5 microns and less) 10 to 100 fine silica, 0.5 to 20 g / l nickel oxalate and NiSO 4 · 6H 2 O 200 to 300
NiCl2 · 6 H2O 40 bisNiCl 2 · 6 H 2 O 40 bis
H3BO3 H 3 BO 3
o-Benzoylsulfimid 1 biso-Benzoyl sulfimide 1 bis
p-Toluolsulfonamid 1 bisp-toluenesulfonamide 1 bis
Allylsulfonsäure 1 bisAllylsulfonic acid 1 bis
2-Butinoxy-l, 4-Diäthansulfonsäure 0,05 bis 0,22-butynoxy-1,4-diethanesulfonic acid 0.05 to 0.2
pH = 3,5 bis 5,5, Badtemperatur 50 bis 700C.pH = 3.5 to 5.5, bath temperature 50 to 70 0 C.
Das Bad kann durch Luft oder mechanisch bewegt werdenThe bath can be moved by air or mechanically
g/lg / l
Nickeloxalat 1 bisNickel oxalate 1 bis
Kieselsäurepulver 30 bisSilica powder 30 to
NiSO4 · 6 H2O 200 bisNiSO 4 · 6 H 2 O 200 to
NiCl2-OH2O 40 bisNiCl 2 -OH 2 O 40 bis
H3BO3 H 3 BO 3
Benzolsulfonamid 2 bisBenzenesulfonamide 2 bis
Allylsulfonsäure 1 bisAllylsulfonic acid 1 bis
N-Allylchinaldinbromid 0,003 bis 0,01N-allyl quinaldine bromide 0.003 to 0.01
pH 4 bis 6; Temperatur 50 bis 70° C.pH 4 to 6; Temperature 50 to 70 ° C.
Beispiel III LuftbewegungExample III Air Movement
g/ig / i
Oxyde der Seltenen Erden (durchschnittliche Partikelgröße, 5 Mikron und weniger) 0,5 bisRare earth oxides (average particle size, 5 microns and less) 0.5 to
Ceroxalat (durchschnittliche Partikelgröße, 5 Mikron und weniger) 0,5 bisCerium oxalate (average particle size, 5 microns and less) 0.5 to
NiSO4 · 6 H2O 200 bisNiSO 4 · 6 H 2 O 200 to
NiCl2-OH2O 40 bisNiCl 2 -OH 2 O 40 bis
H3BO3 H 3 BO 3
o-Benzoylsulfimid 1 biso-Benzoyl sulfimide 1 bis
Benzolsulfonamid 1 bisBenzenesulfonamide 1 bis
Allylsulfonsäure 1 bisAllylsulfonic acid 1 bis
2-Butinoxyl, 4-Diäthansulfonsäure 0,05 bis 0,22-butynoxyl, 4-diethanesulfonic acid 0.05 to 0.2
pH 3,5 bis 5,2; Badtemperatur 50 bis 70° C.pH 3.5 to 5.2; Bath temperature 50 to 70 ° C.
Beispiel IV Luftbewegung oder mechanische BewegungExample IV Air movement or mechanical movement
g/lg / l
Ceroxalat (durchschnittliche Partikelgröße, 5 Mikron und weniger) 0,5 bisCerium oxalate (average particle size, 5 microns and less) 0.5 to
NiSO4 · 6 H2O 200 bisNiSO 4 · 6 H 2 O 200 to
NiCl2-OH2O 30 bisNiCl 2 -OH 2 O 30 bis
H3BO3 Bromal- und/oder Chloralhydrat 0,05 bis 0,1H 3 BO 3 bromal and / or chloral hydrate 0.05 to 0.1
Formaldehyd 0,02 bis 0,08Formaldehyde 0.02 to 0.08
pH 3,5 bis 5,2; Badtemperatur 45 bis 65° C.pH 3.5 to 5.2; Bath temperature 45 to 65 ° C.
Luftbewegung bei Werkstücken auf Gestellen, mechanische Bewegung bei Galvanisierung in TrommelnAir movement for workpieces on racks, mechanical movement for electroplating in drums
g/lg / l
Magnetit (durchschnittliche Partikelgröße, 5 Mikron und weniger) 0,5 bis 5,0Magnetite (average particle size, 5 microns and less) 0.5 to 5.0
ίο Kieselsäure (etwa 0,015 Mikron, äußerste Partikelgröße und durchschnittliche Partikelgröße der Agglomerate, 1,5 Mikron) 40 bis 50ίο Silica (about 0.015 microns, outermost particle size and average Particle size of the agglomerates, 1.5 microns) 40 to 50
NiSO4 · 6 H2O 100 bisNiSO 4 · 6 H 2 O 100 bis
NiCl2-OH2O 40 bisNiCl 2 -OH 2 O 40 bis
H3BO3 40H 3 BO 3 40
o-Benzoylsulfimid 1 bis 4o-Benzoyl sulfimide 1 to 4
Benzolsulfonamid 1 bis 2Benzenesulfonamide 1 to 2
Allylsulfonsäure 1 bis 4Allylsulfonic acid 1 to 4
2-Butinoxy-l, 4-Diäthansulfonsäure 0,05 bis 0,22-butynoxy-1,4-diethanesulfonic acid 0.05 to 0.2
pH 3,5 bis 5,2; Badtemperatur 50 bis 70° C.pH 3.5 to 5.2; Bath temperature 50 to 70 ° C.
Beispiel VII — LuftbewegungExample VII - air movement
Beispiel V LuftbewegungExample V air movement
Lanthanumoxalat oder Neodymoxalat oder Oxalat (durchschnittliche Partikelgröße 5 Mikron undLanthanum oxalate or neodymium oxalate or oxalate (average Particle size 5 microns and
weniger) fewer)
Magnetit Magnetite
NiSO4 · 6 H2O NiSO 4 · 6 H 2 O
NiCl2 · 6 H2O NiCl 2 · 6H 2 O
H3BO3 H 3 BO 3
o-Benzoylsulfimid o-benzoyl sulfimide
Benzolsulfonamid Benzenesulfonamide
Allylsulfonsäure Allyl sulfonic acid
2-Butinoxyl, 4-Diäthansulfonsäure pH 3,5 bis 5,2; Badtemperatur 502-butynoxyl, 4-diethansulfonic acid pH 3.5 to 5.2; Bath temperature 50
g/lg / l
g/lg / l
Didymiumoxid 1 bis 10Didymium oxide 1 to 10
Oxalat Seltener Erden (durchschnittliche Partikelgröße, 5 Mikron und weniger) 1 bis 50Rare earth oxalate (average particle size, 5 microns and less) 1 to 50
NiSO4-OH2O 0 bis 50NiSO 4 -OH 2 O 0 to 50
NiCl2 · 6 H2O 150 bisNiCl 2 · 6 H 2 O 150 bis
H3BO3 40H 3 BO 3 40
Nickelsuccinat 0 bis 15 ·Nickel succinate 0 to 15
o-Benzoylsulfimid 1 bis 4o-Benzoyl sulfimide 1 to 4
Benzolsulfonamid 1 bis 2Benzenesulfonamide 1 to 2
Allylsulfonsäure 1 bis 4Allylsulfonic acid 1 to 4
2-Butinoxy-l, 4-Diäthansulfonsäure 0,05 bis 0,2., 2-butynoxy-1,4-diethansulfonic acid 0.05 to 0.2.,
pH 3,5 bis 5,2; Badtemperatur 50 bis 70°C.pH 3.5 to 5.2; Bath temperature 50 to 70 ° C.
Beispiel VIII LuftbewegungExample VIII Air movement
g/lg / l
Thoriumfluorid allein und/oder gemischt mit Thoriumfluoborat, Thoriumfluosilicat, Thoriumfiuoaluminat, Thoriumfluotitanat und Thoriumfluozirconat (durchschnittliche Partikelgröße, 5 Mikron und weniger) 1 bis 50Thorium fluoride alone and / or mixed with thorium fluorate, thorium fluorosilicate, thorium fluoaluminate, Thorium fluotitanate and thorium fluozirconate (average particle size, 5 microns and less) 1 to 50
NiSO4 · 6 H2O 150 bisNiSO 4 · 6 H 2 O 150 to
NiCl2 · 6 H2O 150 bis 50NiCl 2 · 6 H 2 O 150 to 50
H3BO3 H 3 BO 3
4040
o-Benzoylsulfimid 1 bis 4o-Benzoyl sulfimide 1 to 4
Benzolsulfonamid 1 bis 2Benzenesulfonamide 1 to 2
Allylsulfonsäure 1 bis 4Allylsulfonic acid 1 to 4
2-Butinoxy-l, 4-Diäthansulfonsäure 0^05 bis 0,22-butynoxy-1,4-diethansulfonic acid 0 ^ 05 to 0.2
pH 3,5 bis 5,2; Badtemperatur 50 bis 70° C.pH 3.5 to 5.2; Bath temperature 50 to 70 ° C.
Claims (6)
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US28219963A | 1963-03-01 | 1963-03-01 | |
US262191A US3268307A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating and products thereof |
US262200A US3268423A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating |
US262199A US3268308A (en) | 1963-03-01 | 1963-03-01 | Electrodeposition of a corrosion resistant decorative nickel-chromium coating and products thereof |
US302739A US3268424A (en) | 1963-03-01 | 1963-08-16 | Method of depositing a corrosion resistant composite nickel electroplate |
Publications (3)
Publication Number | Publication Date |
---|---|
DE1521065A1 DE1521065A1 (en) | 1969-08-07 |
DE1521065B2 DE1521065B2 (en) | 1973-04-12 |
DE1521065C3 true DE1521065C3 (en) | 1974-11-07 |
Family
ID=27540443
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE1521063A Expired DE1521063C3 (en) | 1963-03-01 | 1964-02-29 | Acid galvanic nickel bath for depositing decorative fine-grained, satin to high-gloss coatings with improved corrosion resistance |
DE1521065A Expired DE1521065C3 (en) | 1963-03-01 | 1964-08-14 | Acid galvanic nickel bath for the deposition of decorative fine-grained, satin to high-gloss coatings with improved corrosion resistance |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE1521063A Expired DE1521063C3 (en) | 1963-03-01 | 1964-02-29 | Acid galvanic nickel bath for depositing decorative fine-grained, satin to high-gloss coatings with improved corrosion resistance |
Country Status (4)
Country | Link |
---|---|
US (4) | US3268423A (en) |
DE (2) | DE1521063C3 (en) |
GB (1) | GB1051685A (en) |
NL (2) | NL6402091A (en) |
Families Citing this family (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3356467A (en) * | 1964-12-28 | 1967-12-05 | Udylite Corp | Article coated with a coelectrodeposit of nickel and plastic particles, an overlayerthereon, and method of making said article |
US3428441A (en) * | 1965-07-28 | 1969-02-18 | Kewanee Oil Co | Article coated with a composite particulate,microporous chromium coating and method of producing said article |
US3471271A (en) * | 1965-08-16 | 1969-10-07 | Udylite Corp | Electrodeposition of a micro-cracked corrosion resistant nickel-chromium plate |
GB1118167A (en) * | 1965-10-23 | 1968-06-26 | Res Holland Nv | Improvements in or relating to the production of microporous chromium deposits |
US3488263A (en) * | 1968-04-22 | 1970-01-06 | Gen Electric | Codeposition of metallics and non-metallics |
US3625821A (en) * | 1968-06-26 | 1971-12-07 | Westinghouse Electric Corp | Fuel-element coating containing burnable poison |
US3657080A (en) * | 1968-09-25 | 1972-04-18 | M & T Chemicals Inc | Mist suppression in electroplating solutions |
US3866289A (en) * | 1969-10-06 | 1975-02-18 | Oxy Metal Finishing Corp | Micro-porous chromium on nickel-cobalt duplex composite plates |
GB1282373A (en) * | 1969-10-15 | 1972-07-19 | A I C Approvvigionamenti Ind C | Nickel-chromium electroplating |
GB1404855A (en) * | 1971-07-28 | 1975-09-03 | Mitsui Mining & Smelting Co | Catalytic purification of exhaust gases |
US3812566A (en) * | 1972-07-03 | 1974-05-28 | Oxy Metal Finishing Corp | Composite nickel iron electroplate and method of making said electroplate |
DE2236443C3 (en) * | 1972-07-25 | 1978-05-24 | Elektroschmelzwerk Kempten Gmbh, 8000 Muenchen | Aqueous bath for the production of metallic coatings which contain non-metallic, finely divided solids |
US3825478A (en) * | 1972-10-30 | 1974-07-23 | Oxy Metal Finishing Corp | Electrolyte and method for electrodepositing microporous chromium-nickel composite coatings |
JPS5618080B2 (en) * | 1973-08-14 | 1981-04-25 | ||
US4182412A (en) * | 1978-01-09 | 1980-01-08 | Uop Inc. | Finned heat transfer tube with porous boiling surface and method for producing same |
US4470897A (en) * | 1983-09-20 | 1984-09-11 | Bethlehem Steel Corp. | Method of electroplating a corrosion-resistant zinc-containing deposit |
CA1268139A (en) * | 1984-10-05 | 1990-04-24 | John Foster | Composite electrodeposition including particles of craim.sub.2 where m.sub.2is y, si, ti or rare earth |
JPH0772360B2 (en) * | 1987-07-10 | 1995-08-02 | 日本鋼管株式会社 | Zn-based composite electric steel sheet |
US6045682A (en) * | 1998-03-24 | 2000-04-04 | Enthone-Omi, Inc. | Ductility agents for nickel-tungsten alloys |
WO2006082218A1 (en) * | 2005-02-04 | 2006-08-10 | Siemens Aktiengesellschaft | Surface comprising a microstructure that reduces wettability and method for the production thereof |
DE102007060906B3 (en) * | 2007-12-14 | 2009-10-15 | Ab Skf | Bearing arrangement for a carrying roller |
EP2145986B1 (en) * | 2008-07-15 | 2010-03-24 | Atotech Deutschland Gmbh | Solution and method for electrochemically depositing a metal on a substrate |
DE102010055968A1 (en) | 2010-12-23 | 2012-06-28 | Coventya Spa | Substrate with corrosion-resistant coating and process for its preparation |
KR101594723B1 (en) | 2011-08-18 | 2016-02-16 | 애플 인크. | Anodization and plating surface treatments |
KR20130126233A (en) * | 2012-05-11 | 2013-11-20 | 현대자동차주식회사 | Plating method using a intaglio process of multilayer nickel |
GB201308473D0 (en) * | 2013-05-10 | 2013-06-19 | Authentix Inc | Plating of articles |
CN109107559B (en) * | 2018-08-31 | 2021-08-03 | 四川文理学院 | Method for preparing calcium titanate by electrodeposition and application thereof |
CN111926354A (en) * | 2020-10-12 | 2020-11-13 | 江西科技学院 | Electric element for computer data processing device and manufacturing method thereof |
CN116005157B (en) * | 2022-12-13 | 2023-12-19 | 苏州圆格电子有限公司 | Neodymium iron boron surface pretreatment method and system |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2771409A (en) * | 1953-02-19 | 1956-11-20 | Gen Motors Corp | Method of making grid bearings |
US2739085A (en) * | 1953-03-13 | 1956-03-20 | Westinghouse Electric Corp | Insulating coatings for magnetic sheets |
US2849353A (en) * | 1955-02-08 | 1958-08-26 | Hanson Van Winkle Munning Co | Bright nickel plating |
US3057048A (en) * | 1958-11-06 | 1962-10-09 | Horizons Inc | Protection of niobium |
US3061525A (en) * | 1959-06-22 | 1962-10-30 | Platecraft Of America Inc | Method for electroforming and coating |
US3090733A (en) * | 1961-04-17 | 1963-05-21 | Udylite Res Corp | Composite nickel electroplate |
US3132928A (en) * | 1962-02-26 | 1964-05-12 | Donald D Crooks | Simultaneous brazing and corrosion protecting refractory metals |
-
0
- GB GB1051685D patent/GB1051685A/en active Active
-
1963
- 1963-03-01 US US262200A patent/US3268423A/en not_active Expired - Lifetime
- 1963-03-01 US US262191A patent/US3268307A/en not_active Expired - Lifetime
- 1963-03-01 US US262199A patent/US3268308A/en not_active Expired - Lifetime
- 1963-08-16 US US302739A patent/US3268424A/en not_active Expired - Lifetime
-
1964
- 1964-02-29 DE DE1521063A patent/DE1521063C3/en not_active Expired
- 1964-03-02 NL NL6402091A patent/NL6402091A/xx unknown
- 1964-08-14 NL NL6409430A patent/NL6409430A/xx unknown
- 1964-08-14 DE DE1521065A patent/DE1521065C3/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
NL6402091A (en) | 1964-09-02 |
DE1521065B2 (en) | 1973-04-12 |
DE1521063A1 (en) | 1969-08-14 |
NL6409430A (en) | 1965-02-17 |
US3268307A (en) | 1966-08-23 |
DE1521065A1 (en) | 1969-08-07 |
DE1521063B2 (en) | 1974-01-10 |
US3268308A (en) | 1966-08-23 |
GB1051685A (en) | |
US3268424A (en) | 1966-08-23 |
US3268423A (en) | 1966-08-23 |
DE1521063C3 (en) | 1974-08-29 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C3 | Grant after two publication steps (3rd publication) | ||
E77 | Valid patent as to the heymanns-index 1977 | ||
EGZ | Application of addition ceased through non-payment of annual fee of main patent |